US4418204A - Method for making esters - Google Patents

Method for making esters Download PDF

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Publication number
US4418204A
US4418204A US06/422,253 US42225382A US4418204A US 4418204 A US4418204 A US 4418204A US 42225382 A US42225382 A US 42225382A US 4418204 A US4418204 A US 4418204A
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US
United States
Prior art keywords
esters
ester
acid
vacuum
epoxy
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Expired - Lifetime
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US06/422,253
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English (en)
Inventor
Peter J. Arndt
Joachim Lowitz
Manfred Muller
Fritz Schlosser
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Roehm GmbH Darmstadt
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Roehm GmbH Darmstadt
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Assigned to ROHM GMBH reassignment ROHM GMBH ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: ARNDT, PETER J., LOWITZ, JOACHIM, MUELLER, MANFRED, SCHLOSSER, FRITZ
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Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D303/00Compounds containing three-membered rings having one oxygen atom as the only ring hetero atom
    • C07D303/02Compounds containing oxirane rings
    • C07D303/12Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms
    • C07D303/16Compounds containing oxirane rings with hydrocarbon radicals, substituted by singly or doubly bound oxygen atoms by esterified hydroxyl radicals

Definitions

  • One process for the preparation of glycidyl esters is based on a reaction of the sodium or potassium salt of acrylic or methacrylic acid with epichlorohydrin (U.S. Pat. Nos. 2,556,075 and 2,537,981), optionally with the addition of catalytic amounts of tetramethylammonium chloride.
  • the charge may further contain auxiliary agents such as stabilizers, for example, hydroquinone monomethyl ether, hydroquinone, phenothiazine, or N,N'-diphenyl-para-phenylenediamine.
  • auxiliary agents such as stabilizers, for example, hydroquinone monomethyl ether, hydroquinone, phenothiazine, or N,N'-diphenyl-para-phenylenediamine.
  • the process may be carried out in the following manner, for example:
  • the alcohol distillate (methyl methacrylate in azeotropic mixture with methanol) starts to pass over at an overhead temperature of about 30° to 36° C. As soon as no further alcohol distillate is observed, excess methyl methacrylate is drawn off at an increased overhead temperature (about 50° C.).
  • the residual crude ester can be substantially degassed, that is to say, freed of methyl methacrylate. The degassed crude ester can then be vacuum distilled. A pure product is obtained in a very good yield.
  • a mixture of 70.0 kg (945 moles) of glycidol, 280 kg (2800 moles) of methyl methacrylate, 120 ppm of 1,4-diazabicyclo(2,2,2)octane, 30 ppm of KOH (in methanol), and 200 ppm of N,N'-diphenyl-para-phenylenediamine (as a stabilizer) is charged into a 500-liter V4A agitated vessel having a 4-meter steel column packed with porcelain Raschig rings and equipped with water and brine reflux condenser, interchangeable receiver, reflux control, and vacuum control. A vacuum is produced and the vessel is heated by means of circulating hot water. At a vessel temperature of 60° C.
  • a distillate starts passing over from the alcoholysis with a reflux ratio of 2:1.
  • the vessel temperature rises to 70° C., and the overhead temperature is held between 33° and 36° C. by adjustment of the reflux ratio of 5:1.
  • unreacted methyl methacrylate is withdrawn at a reflux ratio of 1:1 and a temperature of 50° C.
  • the crude glycidyl methacrylate ester formed can be degassed down to a residual gas content of about 10%. After further degassing at 110° C.
  • the ester formed in the vapor space and a vacuum of 30 mm Hg, can be distilled at 115° C. in the vapor space and 1 to 2 mm Hg. Yields over 80% are observed.
  • the total time usually ranges from about 6 to 9 hours.
  • a mixture of 475 g (6,41 moles) of glycidol, 2000 g (20 Mol) of methyl methacrylate 200 ppm of 1,4-diazabicyclo(2,2,2)octane and 200 ppm of N,N'-diphenyl-p-phenylenediamine (as a stabilizer) is charged into a 4-liter agitated glass vessel having a 1 meter glass column packed with glass Raschig rings and equipped with a water and a brine reflux condenser, interchangeable receiver, reflux control and vacuum control. A vacuum is produced and the vessel is heated by means of circulating hot water. At a vessel temperature of 60° C.
  • a distillate starts passing over from the alcoholysis with a reflux ratio of 2:1.
  • the vessel temperature rises to 70° C., and the overhead temperature is held between 33° and 36° C. by adjustment of the reflux ratio of 5:1.
  • unreacted methyl methacrylate is withdrawn at a reflux ratio of 1:1 and a temperature of 50° C.
  • the crude glycidyl methacrylate ester formed can be degassed down to a residual gas content of about 10%. After further degassing at 110° C.
  • the ester formed in the vapor space and a vacuum of 30 mm Hg, can be distilled at 115° C. in the vapor space and 1 and 2 mm Hg. Yields over 80% are observed.
  • the total time usually ranges from about 6 to 9 hours.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Epoxy Compounds (AREA)
US06/422,253 1981-10-14 1982-09-23 Method for making esters Expired - Lifetime US4418204A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3140764 1981-10-14
DE19813140764 DE3140764A1 (de) 1981-10-14 1981-10-14 Verfahren zur herstellung der ester vopn carbonsaeuren mit epoxigruppenhaltigen alkoholen

Publications (1)

Publication Number Publication Date
US4418204A true US4418204A (en) 1983-11-29

Family

ID=6144064

Family Applications (1)

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US06/422,253 Expired - Lifetime US4418204A (en) 1981-10-14 1982-09-23 Method for making esters

Country Status (6)

Country Link
US (1) US4418204A (enrdf_load_stackoverflow)
JP (1) JPS5872576A (enrdf_load_stackoverflow)
DE (1) DE3140764A1 (enrdf_load_stackoverflow)
FR (1) FR2514356B1 (enrdf_load_stackoverflow)
GB (1) GB2107319B (enrdf_load_stackoverflow)
IT (1) IT1156520B (enrdf_load_stackoverflow)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5527927A (en) * 1994-05-20 1996-06-18 Mitsubishi Gas Chemical Company, Inc. Process for producing glycidyl acrylate or glycidyl methacrylate
CN103214435A (zh) * 2013-03-20 2013-07-24 沈阳金久奇科技有限公司 一种制备甲基丙烯酸缩水甘油酯的方法

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2537981A (en) * 1949-10-28 1951-01-16 American Cyanamid Co Method of producing a glycidyl ester
US2556075A (en) * 1948-06-19 1951-06-05 American Cyanamid Co Method of polymerizing glycidyl compounds
GB1118206A (en) 1964-12-22 1968-06-26 British Petroleum Co Preparation of epoxy esters
FR2088971A5 (en) 1970-04-30 1972-01-07 Ugilor Methacrylic and acrylic esters - from higher alcohols by transesterification using thallium alcoholate catalyst
DE2602157A1 (de) 1975-01-24 1976-07-29 Ciba Geigy Ag Verfahren zur herstellung von polycarbonsaeurepolyglycidylestern
US4074062A (en) * 1975-08-21 1978-02-14 Mitsubishi Rayon Company, Limited Process for producing unsaturated carboxylic acid esters
US4228084A (en) * 1975-06-05 1980-10-14 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for the production of glycidyl methacrylate
US4285872A (en) * 1977-06-06 1981-08-25 Nippon Oil And Fats Company, Ltd. Method for producing glycidyl (metha)acrylate
DE2423405C3 (de) 1974-05-14 1983-05-19 Degussa Ag, 6000 Frankfurt Verfahren zur Herstellung von Glycidylmethacrylat

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2556075A (en) * 1948-06-19 1951-06-05 American Cyanamid Co Method of polymerizing glycidyl compounds
US2537981A (en) * 1949-10-28 1951-01-16 American Cyanamid Co Method of producing a glycidyl ester
GB1118206A (en) 1964-12-22 1968-06-26 British Petroleum Co Preparation of epoxy esters
FR2088971A5 (en) 1970-04-30 1972-01-07 Ugilor Methacrylic and acrylic esters - from higher alcohols by transesterification using thallium alcoholate catalyst
DE2423405C3 (de) 1974-05-14 1983-05-19 Degussa Ag, 6000 Frankfurt Verfahren zur Herstellung von Glycidylmethacrylat
DE2602157A1 (de) 1975-01-24 1976-07-29 Ciba Geigy Ag Verfahren zur herstellung von polycarbonsaeurepolyglycidylestern
US4228084A (en) * 1975-06-05 1980-10-14 Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler Process for the production of glycidyl methacrylate
US4074062A (en) * 1975-08-21 1978-02-14 Mitsubishi Rayon Company, Limited Process for producing unsaturated carboxylic acid esters
US4285872A (en) * 1977-06-06 1981-08-25 Nippon Oil And Fats Company, Ltd. Method for producing glycidyl (metha)acrylate

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5527927A (en) * 1994-05-20 1996-06-18 Mitsubishi Gas Chemical Company, Inc. Process for producing glycidyl acrylate or glycidyl methacrylate
CN103214435A (zh) * 2013-03-20 2013-07-24 沈阳金久奇科技有限公司 一种制备甲基丙烯酸缩水甘油酯的方法

Also Published As

Publication number Publication date
DE3140764A1 (de) 1983-04-28
GB2107319B (en) 1985-09-11
FR2514356A1 (fr) 1983-04-15
DE3140764C2 (enrdf_load_stackoverflow) 1990-03-01
JPS5872576A (ja) 1983-04-30
GB2107319A (en) 1983-04-27
JPH0321027B2 (enrdf_load_stackoverflow) 1991-03-20
FR2514356B1 (fr) 1987-04-24
IT8268081A0 (it) 1982-09-10
IT1156520B (it) 1987-02-04

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